US2540962A - Process for producing polytetrahaloethylene films - Google Patents
Process for producing polytetrahaloethylene films Download PDFInfo
- Publication number
- US2540962A US2540962A US60338A US6033848A US2540962A US 2540962 A US2540962 A US 2540962A US 60338 A US60338 A US 60338A US 6033848 A US6033848 A US 6033848A US 2540962 A US2540962 A US 2540962A
- Authority
- US
- United States
- Prior art keywords
- sheet
- films
- particles
- resin
- polytetrahaloethylene
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title claims description 23
- 239000011347 resin Substances 0.000 claims description 53
- 229920005989 resin Polymers 0.000 claims description 53
- 239000002245 particle Substances 0.000 claims description 49
- 239000002184 metal Substances 0.000 claims description 21
- 229910052751 metal Inorganic materials 0.000 claims description 21
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 18
- -1 HYDROXY GROUP Chemical group 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 12
- 150000001875 compounds Chemical class 0.000 claims description 10
- 238000001816 cooling Methods 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 10
- 229910052742 iron Inorganic materials 0.000 claims description 9
- 238000000151 deposition Methods 0.000 claims description 8
- 239000010408 film Substances 0.000 description 33
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 26
- 239000010949 copper Substances 0.000 description 26
- 229910052802 copper Inorganic materials 0.000 description 25
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 12
- 239000000725 suspension Substances 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 239000010409 thin film Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 9
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 9
- 239000004810 polytetrafluoroethylene Substances 0.000 description 9
- 238000000576 coating method Methods 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- 239000011248 coating agent Substances 0.000 description 5
- 238000005245 sintering Methods 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000007900 aqueous suspension Substances 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 239000003039 volatile agent Substances 0.000 description 3
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000007598 dipping method Methods 0.000 description 2
- 235000019441 ethanol Nutrition 0.000 description 2
- WWZKQHOCKIZLMA-UHFFFAOYSA-N octanoic acid Chemical compound CCCCCCCC(O)=O WWZKQHOCKIZLMA-UHFFFAOYSA-N 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 125000006850 spacer group Chemical group 0.000 description 2
- 239000005635 Caprylic acid (CAS 124-07-2) Substances 0.000 description 1
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 description 1
- 235000011054 acetic acid Nutrition 0.000 description 1
- 230000001464 adherent effect Effects 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- KRVSOGSZCMJSLX-UHFFFAOYSA-L chromic acid Substances O[Cr](O)(=O)=O KRVSOGSZCMJSLX-UHFFFAOYSA-L 0.000 description 1
- 230000002844 continuous effect Effects 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 229910000431 copper oxide Inorganic materials 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 229940031098 ethanolamine Drugs 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- AWJWCTOOIBYHON-UHFFFAOYSA-N furo[3,4-b]pyrazine-5,7-dione Chemical compound C1=CN=C2C(=O)OC(=O)C2=N1 AWJWCTOOIBYHON-UHFFFAOYSA-N 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 150000002440 hydroxy compounds Chemical class 0.000 description 1
- 239000006194 liquid suspension Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- DUWWHGPELOTTOE-UHFFFAOYSA-N n-(5-chloro-2,4-dimethoxyphenyl)-3-oxobutanamide Chemical compound COC1=CC(OC)=C(NC(=O)CC(C)=O)C=C1Cl DUWWHGPELOTTOE-UHFFFAOYSA-N 0.000 description 1
- 229960002446 octanoic acid Drugs 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- 239000012260 resinous material Substances 0.000 description 1
- 235000019333 sodium laurylsulphate Nutrition 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
- C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
- C08J2327/12—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
- C08J2327/18—Homopolymers or copolymers of tetrafluoroethylene
Definitions
- This invention relates to a process for producing thin films of plastic materials and, more specifically, refers to a process for producing thin films of resins which are not soluble or moldable under ordinary conditions.
- Polytetrafiuoroethylene is an unusual resin, possessing flexibility, extreme solvent resistance, excellent dielectric properties and, generally, exceptional physical and chemical stability. It is, therefore, very useful in many applications where organic resins were heretofore unsatisfactory. Unfortunately, however, it is very difficult to mold, form and extrude. Since it is not soluble in the ordinary solvents or capable of extrusion, the preparation of thin films thereof has heretofore been accomplished by shaving a film from a massive block or cylinder of the material. It is diflicult to obtain uniform film thicknesses by this method and, at best, the thickness of the film is greater than 0.001".
- Films of such thickness are not particularly useful in the manufacture of electrical condensers, which normally employ dielectric spacers of thicknesses on the order of 0.0003". For low voltage operations it is not necessary to employ dielectric thicknesses greater than 0.0005", particularly with a material of high breakdown voltage, such as polytetrafiuoroethylsne.
- the invention is concerned with a process for producing films of polytetrafiuoroethylene which comprises depositing a suspension of particles of polytetrafiuoroethylene in a liquid medium which will react with copper between about 100 C. and 400 C. upon a flexible copper sheet, heating the so coated sheet to a temperature between about 325 C. and about 400 C.
- the invention is concerned with a process for producing films of polytetraiiuoroethylene of a thickness less than about 0.001", which comprises depositing an aqueous suspension of particles of polytetrafiuoroethylene upon a. clean, flexible copper sheet, said particles being less than about 50 microns in diameter, heating the so coated sheet to'about 350 C. for about 1 minute, cooling the resultant laminated sheet, and then stripping of! from the underlying copper sheet the thin film of sintered polytetrafluoroethylene particles, thatis formed.
- volatilizable, hydroxy-groupcontaining compound I am not fully aware of the role played by the volatilizable, hydroxy-groupcontaining compound, but it apparently reacts with the metal base to produce a weak, unbonded thin oxide film to which the sintered resin particles and/or the base metal do not adhere. Alternately or in addition thereto it may produce, at or below the sintering temper ature, a thin, gaseous cushion between the resin and the base, preventing bonding therebetween. In any event, I have found that the presence of the volatilizable, hydroxy group containing compound in the resin layer to be treated leads to the formation of desirable films that may be stripped from the metal base without tearing or appreciable stretching.
- the materials that may be used are methyl alcohol, ethyl alcohol, ethylene glycol, glycerin, acetic acid, propanoic acid, caprylic acid, malonic acid, ethanol amine, etc.
- the resin is preferably a polytetrahaloethylene resin, such as polytetrafiuoroethylene, polytrifluorochloroethylene, and polytetrachloroethylene.
- a polytetrahaloethylene resin such as polytetrafiuoroethylene, polytrifluorochloroethylene, and polytetrachloroethylene.
- the invention may be practiced with other similar resinous materials, if so desired.
- particles of the resin are preferably suspended in a suitable liquid medium, which contains one or more hydroxy-group-containing compounds, such as water, ethyl alcohol or mixtures of these.
- the suspension may be produced by polymerizing the monomeric material in the medium or by milling particles of the resin into the medium with the aid of a dispersing agent, such as sodium lauryl sulfate. In most cases, it is preferable to employ resin particles of a diameter not greater than 50 microns. The sintering of the resin particles and volatilization of other constituents not previously removed may be effected between 300 C. and 400 C.
- the hydroxy material to be deposited along with the resin particles and the liquid suspension medium preferably employed are generally the same or similar compounds. This is desirable, but need not always hold true.
- An emulsion of water and benzene, holding resin particles in suspension may be employed, for example.
- the hydroxy compound should have a higher volatilization point than the boiling point of the suspension medium, as a general rule.
- the preferred embodiment of the invention is concerned with the use of water both for suspending the resin particles and for making the film formed readily removable from the base.
- the surface of the base should be smooth and be composed of clean metal, and the base is preferably flexible, so that the process may be carried out on a continuous basis.
- Suitable metals are those which readily oxidize, such as iron and copper. The latter metal has been found to be particularly satisfactory for the process of the invention.
- the metal surface Prior to the coating of the metal surface with the resin particles and other constituents of the mixture, the metal surface should be cleaned to remove any oil, dirt and loose oxide scale. Acid cleaning is satisfactory for this pur ose.
- the resin film may b stripped from the underlying base and wound on a suitable spool or form adherent oxide particles may be removed by treatment with acid.
- the film will be thin, tough and flexible.
- Figure 1 shows a copper base with a coating or resin particles and water.
- Figure 2 shows the film of sintered resin particles, partially removed from the base.
- FIG. 3 is a schematic diagram of the process of the invention.
- a sheet of copper Ii is unrolled from spool l and passes under reversing pulley II in a cleaning cell l3.
- Acid I4 is contained therein to clean the surface of the copper sheet.
- the sheet passes over pulley l5 and between washing nozzles l6 and I6. These nozzles spray water onto sheet H to wash off and remove any residual acid.
- the sheet then passes over pulley l1 into a coating cell l9, and under reversing pulley l8.
- Cell I9 contains a dispersion or suspension 20 of fine polytetrahaloethylene particles in water. The particles and water deposit on the sheet ll.
- the so coated sheet immediately passes through oven 2
- the laminated sheet formed then passes through stripping tool 22 which separates the copper sheet H from the resin films 23 and 24' which have been produced thereon.
- the resin films 23 and 24 are wound on spools 25 and 21, respectively, while the copper sheet is wound on spool 26 or returned to spool III as a continuou strip.
- a, smooth copper base was cleaned in chromic acid, washed in water, dipped in an aqueous suspension containing 55% by weight of polytetrafiuoroethylene particles having a diameter less than about 20 microns.
- the base was removed from the suspension, with a thin coating of resin particles and water, and then immediately heated to about 370 C. for 4 minutes. After cooling, the resin fihn was readily lifted from the surface of the copper base. It was clear, flexible and tough. Its thickness was about 0.0002". Heavier coatings and hence thicker films may be produced by increasing the resin content of the suspension and/or by increasing the resin particle size.
- temperatures between about 300 C. and about 400 C. are suitable for the polytetrahaloethylene resins, with sintering times varying between about 5 seconds and about 10 minutes.
- the films of the invention are very useful as dielectric spacers for electrical condensers, combining the desirable properties of flexibility, inertness, low loss and temperature resistance without the thickness associated with prior polytetrahaloethylene films.
- a process for producing films of polytetrahaloethylene resins less than 0.0001 inch thick comprises depositing a mixture of poiytetrahaloethylene resin particles less than 50 microns in diameter and a volatilizable liquid compound containing a hydroxy group upon a smooth surface of a sheet of metal selected from the class consisting of iron and copper, heating the metal surface and the mixture deposited thereon to a temperature between about 300 C. and about 400 C. for at least about 5 seconds to sinter the resin particles together, cooling them, and then stripping off from the underlying metal surface the film of sintered resin particles so formed.
- a process for producing thin films of polytetrafluoroethylene which comprises dipping a smoothly surfaced sheet of a metal selected from the class consisting of copper and iron, in a suspension of particles of polytetrafluoroethylene resin less than 50 microns in diameter in a liquid, volatile compound containing a hydroxy group to coat the sheet with a layer of said suspension, heating the so coated sheet to a temperature between about 325 C. and about 400 C. for a about 10 the film, they may be removed by treatment minutes to sinter the particles together, cooling the resultant laminated sheet, and then strippin oi! from the underlying copper sheet the film of sintered polytetrafiuoroethylene particles, that is formed.
- a process for producing thin films of polytetrafluoroethylene of a thickness less than about 0.001 which comprises depositing an aqueous suspension of particles of polytetrafiuoroethylene upon a clean, flexible copper sheet, said particles being less than about 50 microns in diameter, immediately heating the so coated sheet to about 350 C. for about 1 minute, cooling the resultant laminated sheet, and then stripping off from the underlying copper sheet the thin film of sintered polytetrafluoroethylene particles, that is formed.
- a process for producing thin films of polytetrahaloethylene resin which comprises depositing a mixture of polytetrahaloethylene resin particles and a volatilizable compound containing a hydroxy group upon a smooth surface of a metal selected from the class consisting 01' iron and copper, heating the metal surface and the mixture deposited thereon to a temperature between about 300 C. and about 400 C. for at least about five seconds to sinter the resin particles together, cooling them, and then stripping off from the underlying metal surface the film of sintered resin particles so formed, the above sequence of steps being entirely carried out at substantially atmospheric pressure.
- a process for producing thin films of polytetrahaloethylene resins which comprises dipping a smooth sheet of a metal of the class consistin 0! copper and iron into a suspension of polytetrafiuoroethylene particle less than 50 microns in diameter in a liquid volatile compound that contains a hydroxy group, to coat both sides of the sheet with the suspension, heating the coated sheet to volatilize the liquid and sinter the resin particles together into continuous films on each side of the sheet, cooling the resulting combination, and then stripping oft both films from the sheet.
- a continuous process for producing thin films of polytetrafluoroethylene which comprises passing a smooth continuous sheet of a metal selected from the class consisting of iron and copper through a suspension of particles of polytetrafluoroethylene resin in a liquid volatile compound containing a hydroxy group, thus coating both sides of the sheet with a mixture of the resin particles and the liquid, then passing the socoated sheet through a zone in which it is heated to a temperature between about 325 C. and about 400 C.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Laminated Bodies (AREA)
Description
Feb. 6, 1951 H. F. PUPPOLO 2,540,962
PROCESS FOR PRODUCING POLYTETRAHALOETHYLENE FILMS Filed Nov. 16, 1948 Rea/N FILM F/& I iii? F76. 2
Will/[Id Willi/[IA HENRY F. Farm/.0
INVENTOR.
Patented Feb. 6, 1951 2,540,962 PROCESS FOR PRODUCING POLYTETRA- HALOETHYL Henry F. Puppolo,
ENE
North Adams, Masa, assignor FILMS to Sprague Electric Company, North Adams, Masa, a corporation of Massachusetts Application November 16, 1948, Serial No. 00,338
7 Claims. 1
This invention relates to a process for producing thin films of plastic materials and, more specifically, refers to a process for producing thin films of resins which are not soluble or moldable under ordinary conditions.
Polytetrafiuoroethylene is an unusual resin, possessing flexibility, extreme solvent resistance, excellent dielectric properties and, generally, exceptional physical and chemical stability. It is, therefore, very useful in many applications where organic resins were heretofore unsatisfactory. Unfortunately, however, it is very difficult to mold, form and extrude. Since it is not soluble in the ordinary solvents or capable of extrusion, the preparation of thin films thereof has heretofore been accomplished by shaving a film from a massive block or cylinder of the material. It is diflicult to obtain uniform film thicknesses by this method and, at best, the thickness of the film is greater than 0.001". Films of such thickness are not particularly useful in the manufacture of electrical condensers, which normally employ dielectric spacers of thicknesses on the order of 0.0003". For low voltage operations it is not necessary to employ dielectric thicknesses greater than 0.0005", particularly with a material of high breakdown voltage, such as polytetrafiuoroethylsne.
It is an object of the present invention to overcome the foregoing and related disadvantages of prior art procedures. A further object is to produce very thin, impervious films of polytetrahaloethylene resins by a simple process. Additional objects will become apparent from the following description and claims.
These objects are attained in accordance with the present invention by utilizing a process which comprises depositing a mixture of polytetrahaloethylene resin particles and a volatilizable compound containing a hydroxyl group upon a smooth surface of a metal selected from the class containing iron and copper, heating the metal surface and mixture deposited thereon to a temperature between about 300 C. and about 400 C., cooling them, and then stripping off from the underlying metal surface the him of sintered resin particles 50 formed. In a more restricted sense, the invention is concerned with a process for producing films of polytetrafiuoroethylene which comprises depositing a suspension of particles of polytetrafiuoroethylene in a liquid medium which will react with copper between about 100 C. and 400 C. upon a flexible copper sheet, heating the so coated sheet to a temperature between about 325 C. and about 400 C.
for a period between about 5 seconds and about minutes, cooling the resultant laminated sheet, and then stripping off from the underlying copper sheet the film of sintered polytetrafluoroethylene particles, that is formed. In one of its preferred embodiments, the invention is concerned with a process for producing films of polytetraiiuoroethylene of a thickness less than about 0.001", which comprises depositing an aqueous suspension of particles of polytetrafiuoroethylene upon a. clean, flexible copper sheet, said particles being less than about 50 microns in diameter, heating the so coated sheet to'about 350 C. for about 1 minute, cooling the resultant laminated sheet, and then stripping of! from the underlying copper sheet the thin film of sintered polytetrafluoroethylene particles, thatis formed.
1 have discovered that it is possible to prepare very thin, uniform films of polytetrahaloethylene resins by producing them under conditions such that the film may readily be stripped from the base material upon which it is formed. This involves depositing a mixture of particles of the resin and a volatilizable material, preferably liquid, containing hydroxy groups upon a clean, flat surface 0! copper or iron. The base and deposited layer are then heated to a temperature at which the resin particles are sintered together, while the hydroxy-group-containing compound is removed by volatilization and/or reaction. I am not fully aware of the role played by the volatilizable, hydroxy-groupcontaining compound, but it apparently reacts with the metal base to produce a weak, unbonded thin oxide film to which the sintered resin particles and/or the base metal do not adhere. Alternately or in addition thereto it may produce, at or below the sintering temper ature, a thin, gaseous cushion between the resin and the base, preventing bonding therebetween. In any event, I have found that the presence of the volatilizable, hydroxy group containing compound in the resin layer to be treated leads to the formation of desirable films that may be stripped from the metal base without tearing or appreciable stretching. While I have specified water as a preferred material, other volatllizable, hydroxy group containing compounds, preferably liquid, may be employed alone or in admixture with water. Representative of the materials that may be used are methyl alcohol, ethyl alcohol, ethylene glycol, glycerin, acetic acid, propanoic acid, caprylic acid, malonic acid, ethanol amine, etc.
The resin is preferably a polytetrahaloethylene resin, such as polytetrafiuoroethylene, polytrifluorochloroethylene, and polytetrachloroethylene. However, the invention may be practiced with other similar resinous materials, if so desired. The
particles of the resin are preferably suspended in a suitable liquid medium, which contains one or more hydroxy-group-containing compounds, such as water, ethyl alcohol or mixtures of these. The suspension may be produced by polymerizing the monomeric material in the medium or by milling particles of the resin into the medium with the aid of a dispersing agent, such as sodium lauryl sulfate. In most cases, it is preferable to employ resin particles of a diameter not greater than 50 microns. The sintering of the resin particles and volatilization of other constituents not previously removed may be effected between 300 C. and 400 C.
It will be noted that the hydroxy material to be deposited along with the resin particles and the liquid suspension medium preferably employed are generally the same or similar compounds. This is desirable, but need not always hold true. An emulsion of water and benzene, holding resin particles in suspension, may be employed, for example. When they differ, the hydroxy compound should have a higher volatilization point than the boiling point of the suspension medium, as a general rule. The preferred embodiment of the invention is concerned with the use of water both for suspending the resin particles and for making the film formed readily removable from the base.
The surface of the base should be smooth and be composed of clean metal, and the base is preferably flexible, so that the process may be carried out on a continuous basis. Suitable metals are those which readily oxidize, such as iron and copper. The latter metal has been found to be particularly satisfactory for the process of the invention. Prior to the coating of the metal surface with the resin particles and other constituents of the mixture, the metal surface should be cleaned to remove any oil, dirt and loose oxide scale. Acid cleaning is satisfactory for this pur ose.
Following the sintering of the resin particles and volatilization and/or reaction of other constituents, the resin film may b stripped from the underlying base and wound on a suitable spool or form adherent oxide particles may be removed by treatment with acid. The film will be thin, tough and flexible.
Reference is now made ing, in which Figure 1 shows a copper base with a coating or resin particles and water.
Figure 2 shows the film of sintered resin particles, partially removed from the base.
Figure 3 is a schematic diagram of the process of the invention. A sheet of copper Ii is unrolled from spool l and passes under reversing pulley II in a cleaning cell l3. Acid I4 is contained therein to clean the surface of the copper sheet. Thereafter, the sheet passes over pulley l5 and between washing nozzles l6 and I6. These nozzles spray water onto sheet H to wash off and remove any residual acid. The sheet then passes over pulley l1 into a coating cell l9, and under reversing pulley l8. Cell I9 contains a dispersion or suspension 20 of fine polytetrahaloethylene particles in water. The particles and water deposit on the sheet ll. Thereafter, the so coated sheet immediately passes through oven 2| which is heated to a temperature sufllcient to sinter the to the appended draw- 7 period between about 5 seconds and particles of resin together. At the same time, most of the water is boiled away, while a minor amount apparently reacts with the copper base, as heretofore described. The laminated sheet formed then passes through stripping tool 22 which separates the copper sheet H from the resin films 23 and 24' which have been produced thereon. The resin films 23 and 24 are wound on spools 25 and 21, respectively, while the copper sheet is wound on spool 26 or returned to spool III as a continuou strip.
If copper or iron oxide particles should adhere to with acid, which dissolves the oxide but does not affect the inert resin film.
As a specific example, a, smooth copper base was cleaned in chromic acid, washed in water, dipped in an aqueous suspension containing 55% by weight of polytetrafiuoroethylene particles having a diameter less than about 20 microns. The base was removed from the suspension, with a thin coating of resin particles and water, and then immediately heated to about 370 C. for 4 minutes. After cooling, the resin fihn was readily lifted from the surface of the copper base. It was clear, flexible and tough. Its thickness was about 0.0002". Heavier coatings and hence thicker films may be produced by increasing the resin content of the suspension and/or by increasing the resin particle size.
The time and temperature of heating are interdependent, as well as dependent upon the particular resin to be treated. As a general rule, temperatures between about 300 C. and about 400 C. are suitable for the polytetrahaloethylene resins, with sintering times varying between about 5 seconds and about 10 minutes.
The films of the invention are very useful as dielectric spacers for electrical condensers, combining the desirable properties of flexibility, inertness, low loss and temperature resistance without the thickness associated with prior polytetrahaloethylene films.
As many widely different embodiments of my invention may be made without departing from the spirit and scope hereof, it is to be understood that it is not limited to the specific embodiments hereof except as defined in the appended claims.
I claim:
1. A process for producing films of polytetrahaloethylene resins less than 0.0001 inch thick, which process comprises depositing a mixture of poiytetrahaloethylene resin particles less than 50 microns in diameter and a volatilizable liquid compound containing a hydroxy group upon a smooth surface of a sheet of metal selected from the class consisting of iron and copper, heating the metal surface and the mixture deposited thereon to a temperature between about 300 C. and about 400 C. for at least about 5 seconds to sinter the resin particles together, cooling them, and then stripping off from the underlying metal surface the film of sintered resin particles so formed.
2. A process for producing thin films of polytetrafluoroethylene which comprises dipping a smoothly surfaced sheet of a metal selected from the class consisting of copper and iron, in a suspension of particles of polytetrafluoroethylene resin less than 50 microns in diameter in a liquid, volatile compound containing a hydroxy group to coat the sheet with a layer of said suspension, heating the so coated sheet to a temperature between about 325 C. and about 400 C. for a about 10 the film, they may be removed by treatment minutes to sinter the particles together, cooling the resultant laminated sheet, and then strippin oi! from the underlying copper sheet the film of sintered polytetrafiuoroethylene particles, that is formed.
3. A process for producing thin films of polytetrafluoroethylene of a thickness less than about 0.001", which comprises depositing an aqueous suspension of particles of polytetrafiuoroethylene upon a clean, flexible copper sheet, said particles being less than about 50 microns in diameter, immediately heating the so coated sheet to about 350 C. for about 1 minute, cooling the resultant laminated sheet, and then stripping off from the underlying copper sheet the thin film of sintered polytetrafluoroethylene particles, that is formed.
4. The process as defined by claim 1 in which the smooth surface is a copper surface.
5. A process for producing thin films of polytetrahaloethylene resin which comprises depositing a mixture of polytetrahaloethylene resin particles and a volatilizable compound containing a hydroxy group upon a smooth surface of a metal selected from the class consisting 01' iron and copper, heating the metal surface and the mixture deposited thereon to a temperature between about 300 C. and about 400 C. for at least about five seconds to sinter the resin particles together, cooling them, and then stripping off from the underlying metal surface the film of sintered resin particles so formed, the above sequence of steps being entirely carried out at substantially atmospheric pressure.
6. A process for producing thin films of polytetrahaloethylene resins which comprises dipping a smooth sheet of a metal of the class consistin 0! copper and iron into a suspension of polytetrafiuoroethylene particle less than 50 microns in diameter in a liquid volatile compound that contains a hydroxy group, to coat both sides of the sheet with the suspension, heating the coated sheet to volatilize the liquid and sinter the resin particles together into continuous films on each side of the sheet, cooling the resulting combination, and then stripping oft both films from the sheet.
'7. A continuous process for producing thin films of polytetrafluoroethylene, which comprises passing a smooth continuous sheet of a metal selected from the class consisting of iron and copper through a suspension of particles of polytetrafluoroethylene resin in a liquid volatile compound containing a hydroxy group, thus coating both sides of the sheet with a mixture of the resin particles and the liquid, then passing the socoated sheet through a zone in which it is heated to a temperature between about 325 C. and about 400 C. for a period between about 5 seconds and about 10 minutes, thus volatilizing the liquid and sintering the resin particles, then passing the resultant laminated sheet through a zone in which it is cooled, and finally passing it through a device wherein the films of sintered polytetrafluoroethylene are continuously stripped off from the underlying metal sheet.
HENRY F. PUPPOLO.
REFERENCES CITED Alfthan Apr. 20, 1948 Staudinger et ai. June 8, 1948 Number
Claims (1)
1. A PROCESS FOR PRODUCING FILMS OF POLYTETRAHALOETHYLENE RESINS LESS THAN 0.0001 INCH THICK, WHICH PROCESS COMPRISES DEPOSITING A MIXTURE OF POLYTETRAHALOETHYLENE RESIN PARTICLES LESS THAN 50 MICRONS IN DIAMETER AND A VOLATILIZABLE LIQUID COMPOUND CONTAINING A HYDROXY GROUP UPON A SMOOTH SURFACE OF A SHEET OF METAL SELECTED FROM THE CLASS CONSISTING OF IRON AND COPPER, HEATING THE METAL SURFACE AND THE MIXTURE DEPOSITED THEREON TO A TEMPERATURE BETWEEN ABOUT 300* C. AND ABOUT 400* C. FOR AT LEAST ABOUT 5 SECONDS TOO SINTER THE RESIN PARTICLES TOGETHER, COOLING THEM, AND THEN STRIPPING OFF FROM THE UNDERLYING METAL SURFACE THE FILM OF SINTERED RESIN PARTICLES SO FORMED.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US60338A US2540962A (en) | 1948-11-16 | 1948-11-16 | Process for producing polytetrahaloethylene films |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US60338A US2540962A (en) | 1948-11-16 | 1948-11-16 | Process for producing polytetrahaloethylene films |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2540962A true US2540962A (en) | 1951-02-06 |
Family
ID=22028880
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US60338A Expired - Lifetime US2540962A (en) | 1948-11-16 | 1948-11-16 | Process for producing polytetrahaloethylene films |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2540962A (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2773050A (en) * | 1952-04-30 | 1956-12-04 | Eastman Kodak Co | Water vapor permeable compositions and articles containing a polyacrylic ester and polyvinyl alcohol |
| US2790999A (en) * | 1951-10-20 | 1957-05-07 | Sprague Electric Co | Process for producing porous polytetrafluoroethylene film |
| US2852811A (en) * | 1954-03-01 | 1958-09-23 | John V Petriello | Method for casting thin plastic films |
| US2859482A (en) * | 1954-07-16 | 1958-11-11 | Dunlop Rubber Co | Belting |
| US2923646A (en) * | 1957-12-12 | 1960-02-02 | Rohm & Haas | Release-coatings, film- and sheetcasting bases for substrates |
| US2961345A (en) * | 1957-08-05 | 1960-11-22 | John V Petriello | Composite plastic film and a method of making the same in continuous form |
| US2980965A (en) * | 1958-02-28 | 1961-04-25 | American Mach & Foundry | Method of making plastic film |
| US3089783A (en) * | 1960-01-06 | 1963-05-14 | Pfaudler Permutit Inc | Corrosion resistant coating and method of applying the same |
| US3311494A (en) * | 1964-12-07 | 1967-03-28 | Gen Electric | Processes of producing smooth adherent coatings of polytetrafluoroethylene |
| US3664888A (en) * | 1965-10-09 | 1972-05-23 | Sumitomo Electric Industries | Method of resin coating a metal and resin-coated metal product thereof |
| US3673292A (en) * | 1968-06-12 | 1972-06-27 | Bosch Gmbh Robert | Process for the preparation of gas permeable hydrophobic foils for electrochemical cells |
| US4374791A (en) * | 1981-09-28 | 1983-02-22 | The Upjohn Company | Process for preparing particleboard |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2440190A (en) * | 1944-03-01 | 1948-04-20 | Du Pont | Preparation of nonporous polytetrafluoroethylene articles |
| US2442940A (en) * | 1944-04-17 | 1948-06-08 | Distillers Co Yeast Ltd | Process for making shaped porous masses of thermoplastic synthetic resinous materials |
-
1948
- 1948-11-16 US US60338A patent/US2540962A/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2440190A (en) * | 1944-03-01 | 1948-04-20 | Du Pont | Preparation of nonporous polytetrafluoroethylene articles |
| US2442940A (en) * | 1944-04-17 | 1948-06-08 | Distillers Co Yeast Ltd | Process for making shaped porous masses of thermoplastic synthetic resinous materials |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2790999A (en) * | 1951-10-20 | 1957-05-07 | Sprague Electric Co | Process for producing porous polytetrafluoroethylene film |
| US2773050A (en) * | 1952-04-30 | 1956-12-04 | Eastman Kodak Co | Water vapor permeable compositions and articles containing a polyacrylic ester and polyvinyl alcohol |
| US2852811A (en) * | 1954-03-01 | 1958-09-23 | John V Petriello | Method for casting thin plastic films |
| US2859482A (en) * | 1954-07-16 | 1958-11-11 | Dunlop Rubber Co | Belting |
| US2961345A (en) * | 1957-08-05 | 1960-11-22 | John V Petriello | Composite plastic film and a method of making the same in continuous form |
| US2923646A (en) * | 1957-12-12 | 1960-02-02 | Rohm & Haas | Release-coatings, film- and sheetcasting bases for substrates |
| US2980965A (en) * | 1958-02-28 | 1961-04-25 | American Mach & Foundry | Method of making plastic film |
| US3089783A (en) * | 1960-01-06 | 1963-05-14 | Pfaudler Permutit Inc | Corrosion resistant coating and method of applying the same |
| US3311494A (en) * | 1964-12-07 | 1967-03-28 | Gen Electric | Processes of producing smooth adherent coatings of polytetrafluoroethylene |
| US3664888A (en) * | 1965-10-09 | 1972-05-23 | Sumitomo Electric Industries | Method of resin coating a metal and resin-coated metal product thereof |
| US3673292A (en) * | 1968-06-12 | 1972-06-27 | Bosch Gmbh Robert | Process for the preparation of gas permeable hydrophobic foils for electrochemical cells |
| US4374791A (en) * | 1981-09-28 | 1983-02-22 | The Upjohn Company | Process for preparing particleboard |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2540962A (en) | Process for producing polytetrahaloethylene films | |
| US2520173A (en) | Process for preparing unsupported films of tetrafluoroethylene polymers | |
| DE69305318T2 (en) | Process for the production of a silicon oxide film | |
| US2852811A (en) | Method for casting thin plastic films | |
| US2689805A (en) | Method of coating polytetrafluoroethylene articles and resulting articles | |
| EP0564911A2 (en) | Antistatic plastic parts | |
| US2999772A (en) | Coated article comprising a substrate of polyethylene or polyamide and a grafted coating of polytetrafluoroethylene or polymethyl methacrylate | |
| DE2161434A1 (en) | ||
| US2865795A (en) | Insulated electrical conductor and method of making the same | |
| DE2513858C3 (en) | Process for the production of a tantalum thin film capacitor | |
| DE3878729T2 (en) | METHOD FOR PRODUCING A METALIZED POLYOLEFIN FILM. | |
| DE2805152A1 (en) | DIELECTRIC COMPOSING AN ORGANIC POLYMERISATE AND PROCESS FOR ITS MANUFACTURING | |
| US2721154A (en) | Production of conducting layers upon electrical insulating materials | |
| US2961345A (en) | Composite plastic film and a method of making the same in continuous form | |
| US2906009A (en) | High temperature-resisting insulating coatings of increased durability and methods of producing same | |
| US2704265A (en) | Electrically conducting films on cast plastics | |
| US2215562A (en) | Method of forming rubber articles | |
| US3673292A (en) | Process for the preparation of gas permeable hydrophobic foils for electrochemical cells | |
| DE1720817A1 (en) | Manufacture of films by ultraviolet surface photopolymerization | |
| US2980965A (en) | Method of making plastic film | |
| US2429861A (en) | Coating compositions of polyethylene and process for applying same | |
| EP0065691A1 (en) | Process for producing a film-like poly(acetylene) | |
| DE2737792C3 (en) | Process for improving the adhesion of poly-p-xylylenes to substrates by applying an organosilane layer | |
| US3262900A (en) | Masking compositions for printed circuits | |
| DE1720890A1 (en) | Manufacture of films by ultraviolet surface photopolymerization |